US4272622A - Method for preventing polymer scale deposition in the polymerization of an ethylenically unsaturated monomer in an aqueous medium - Google Patents

Method for preventing polymer scale deposition in the polymerization of an ethylenically unsaturated monomer in an aqueous medium Download PDF

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Publication number
US4272622A
US4272622A US06/149,414 US14941480A US4272622A US 4272622 A US4272622 A US 4272622A US 14941480 A US14941480 A US 14941480A US 4272622 A US4272622 A US 4272622A
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water
polymerization
soluble
coating solution
polymer compound
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US06/149,414
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Hajime Kitamura
Toshihide Shimizu
Ichiro Kaneko
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Shin Etsu Chemical Co Ltd
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Shin Etsu Chemical Co Ltd
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Priority claimed from JP6278079A external-priority patent/JPS55155002A/ja
Priority claimed from JP6476579A external-priority patent/JPS55157602A/ja
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/002—Scale prevention in a polymerisation reactor or its auxiliary parts
    • C08F2/004—Scale prevention in a polymerisation reactor or its auxiliary parts by a prior coating on the reactor walls

Definitions

  • the present invention relates to a method for preventing polymer scale deposition on reactor walls in the polymerization of an ethylenically unsaturated monomer in an aqueous medium.
  • Ethylenically unsaturated monomers are polymerized in several different ways including suspension or emulsion polymerization in an aqueous medium, solution polymerization, gas-phase polymerization and bulk polymerization according to the kind of the monomer and the desired properties of the polymer.
  • suspension or emulsion polymerization in an aqueous medium solution polymerization
  • gas-phase polymerization gas-phase polymerization
  • bulk polymerization according to the kind of the monomer and the desired properties of the polymer.
  • monomers are almost exclusively polymerized in an aqueous medium. Examples of such monomers are vinyl chloride, vinylidene chloride and styrene.
  • the polymer scale deposition on the reactor walls must be prevented as completely as possible because not only of the decrease in the yield of the polymer product and lowering of the cooling capacity of the reactor but also of the degraded quality of the polymer product due to the intermingled fragments of the polymer scale in the product coming off the reactor walls. Further, the works of removing polymer scale require much time and labor with consequently decreased productivity and increased production costs of the polymer products. What is worse, unreacted monomers are included in a large amount in the polymer scale and the workers undertaking the removal of the scale are exposed to the vapor of the monomer which is very dangerous due to its toxicity to the human health.
  • polymer scale deposition on the reactor walls in the aqueous suspension polymerization of vinyl chloride can be reduced by coating the reactor walls, prior to polymerizaion, with a polar organic compound such as amine compounds, quinone compounds, aldehyde compounds and the like or an organic dye (see, for example, U.S. Pat. No. 3,669,946).
  • a polar organic compound such as amine compounds, quinone compounds, aldehyde compounds and the like or an organic dye
  • This method is considerably effective in preventing polymer scale deposition but the problem in the method is the use of an organic solvent to dissolve the organic compound or the dye which is not or sparingly soluble in water in order to obtain a coating solution.
  • the effectiveness of the above described method is considerably durable when the polymerization of vinyl chloride is carried out as suspension polymerization but, when the polymerization medium contains an emulsifying agent such as in the emulsion polymerization or in the combined use of an emulsifying agent with a suspending agent, effectiveness of the coating method is limited and not durable.
  • Another object of the present invention is to provide a method for preventing polymer scale deposition in the above mentioned types of polymerization by providing a coating layer on the reactor walls prior to polymerization, in which the coating layer is formed by use of an aqueous coating solution so as to be freed from the problems in the prior art method using organic coating solutions.
  • the aqueous coating solution is admixed with an aliphatic monovalent lower alchohol having from 3 to 6 carbon atoms in a molecule so as that the spreadability or wettability of the solution on metal surfaces of the polymerization reactor can be improved.
  • the component (a) contained in the aqueous coating solution is a water-soluble ionic polymer compound which may be either cationic or anionic.
  • the water-soluble cationic polymer compounds as a class of the component (a) on one side are exemplified by those cationic polymer electrolytes containing nitrogen atoms in the main chain or as pendant groups to the polymer main chain where the nitrogen atoms are positively charged or polarized.
  • polymers examples include: polyethyleneimines; polyvinylamines; polyacrylamides; copolymers of N-vinyl-2-pyrrolidone and acrylamide; cyclic polymers of dimethyldiamylammonium chloride; cyclic polymers of dimethyldiethylammonium bromide; cyclic polymers of diallylamine hydrochloride; cyclic copolymers of dimethyldiallylammonium chloride and sulfur dioxide; polyvinyl pyridines; polyvinylpyrrolidones; polyvinylcarbazoles; polyvinylimidazolines; poly(dimethylaminoethyl acrylates); poly(dimethylaminoethyl methacrylates); poly(diethylaminoethyl acrylates); poly(diethylaminoethyl methacrylates) and the like.
  • the water-soluble anionic polymer compounds as the other class of the component (a) on the other side are exemplified by those anionic polymer electrolytes having salt structures of carboxylates or sulfonates with alkali metal ions or ammonium ions in the pendant groups.
  • anionic polymer electrolytes having salt structures of carboxylates or sulfonates with alkali metal ions or ammonium ions in the pendant groups.
  • examples of such polymers are: sulfomethylated polyacrylamides; sodium polyacrylates; sodium alginates; copolymers of acrylamide and sodium vinylsulfonates; sodium polymethacrylates; sodium polystyrenesulfonates; sodium polyethylenesulfonates; sodium ligninsulfonates; sodium chondroitin sulfonates and the like.
  • the water-soluble ionic dyes as the component (b) in the aqueous coating solution used in the inventive method are also divided into two classes of anionic ones and cationic ones. As is mentioned before, the water-soluble anionic dyes are used as combined with the water-soluble cationic polymer compound whereas the water-soluble cationic dyes are used as combined with the water-soluble anionic polymer compound.
  • the water-soluble anionic dyes suitable for use belong to several classes such as water-soluble azo dyes, water-soluble anthraquinone dyes, water-soluble triarylmethane dyes, water-soluble xanthene dyes, water-soluble azine dyes, water-soluble quinoline dyes, water-soluble nitro dyes, water-soluble phthalocyanine dyes and the like.
  • water-soluble anionic dyes belonging to each of the above mentioned classes are as follows.
  • Water-soluble azo dyes C.I. Acid Orange 7; C.I. Acid Red 37; C.I. Acid Red 264; C.I. Acid Blue 1.13; C.I. Acid Black 1; C.I. Acid Yellow 42; C.I. Acid Blue 158; C.I. Acid Green 12; C.I. Acid Orange 97; C.I. Acid Black 124; C.I. Direct Yellow 50; C.I. Direct Red 37; C.I. Direct Red 2; C.I. Direct Violet 12; C.I. Direct Blue 1; C.I. Direct Brown 1; C.I. Direct Black 77; C.I. Direct Green 1; C.I. Direct Orange 26; C.I. Direct Red 79; C.I. Direct Red 31; C.I.
  • Direct Black 32 C.I. Direct Yellow 12; C.I. Direct Orange 41; C.I. Direct Red 113; C.I. Direct Yellow 28; C.I. Direct Green 26; C.I. Direct Red 81; C.I. Direct Violet 51; C.I. Direct Blue 71; C.I. Direct Brown 37; and C.I. Direct Black 19
  • Water-soluble anthraquinone dyes C.I. Acid Blue 40; C.I. Acid Red 80; and C.I. Acid Green 41
  • Water-soluble triarylmethane dyes C.I. Acid Blue 1; C.I. Acid Violet 17; and C.I. Acid Green 16
  • Water-soluble xanthene dyes C.I. Acid Red 87; and C.I. Acid Red 52
  • Water-soluble azine dyes C.I. Acid Blue 59; and C.I. Acid Black 2
  • Water-soluble quinoline dyes C.I. Acid Yellow 3; and C.I. Acid Yellow 7
  • Water-soluble phthalocyanine dyes C.I. Direct Blue 86
  • water-soluble cationic dyes suitable for use in the inventive method are exemplified by water-soluble azine dyes, e.g. C.I. Basic Red 2, C.I. Basic Blue 16 and C.I. Basic Black 2; water-soluble acrydine dyes, e.g. C.I. Basic Orange 14, and C.I. Basic Orange 15; water-soluble triphenylmethane dyes, e.g. C.I. Basic Blue 1, C.I. Basic Violet 3, C.I. Basic Blue 26, C.I. Basic Violet 14, C.I. Basic Blue 5 and C.I. Basic Blue 7; water-soluble thiazine dyes, e.g. C.I. Basic Blue 9, C.I. Basic Yellow 1, C.I.
  • the above described components (a) and (b) have desirably good or moderate solubility in water but they are not required to be highly water-soluble.
  • a compound having a solubility in water of 0.1% by weight or larger can be used suitably for the preparation of the aqueous coating solution.
  • the weight ratio of the individual components (a) and (b) in the aqueous coating solution is of some importance in order to obtain highest effect of scale prevention.
  • the weight ratio of the component (a) to the component (b) is preferably in the range from 100:5 to 100:100 or, more preferably, from 100:15 to 100:50.
  • the amount of the component (b) relative to the amount of the component (a) is in excess over the above defined range, solid precipitates may sometimes be formed so that no satisfactory coating solution is obtained.
  • the concentrations of the components (a) and (b) in the aqueous coating solution is not particularly limitative. It should be noted, however, that the total concentration of the components (a) and (b) is desirably at least 0.01% by weight since, as a matter of course, satisfactory results are not obtained by coating the reactor surfaces with a coating solution too low in the concentrations of the components (a) and (b). On the other hand, no upper limit is given for the concentrations of these components in the coating solution and a solution of any high concentration can be used if the disadvantages accompanying the use of a coating solution of high concentration is disregarded that no particular additional advantages are obtained leading to lowered economy and that, instead, some inconvenience is caused in the application of the coating solution on to the reactor surfaces. Therefore, it is recommended that the total concentration of the components (a) and (b) in the coating solution does not exceed 5% by weight.
  • the aqueous coating solution used in the inventive method is readily prepared by merely disolving the components (a) and (b) in water in the concentrations and in the weight ratio as described above.
  • the thus prepared aqueous coating solution can be applied as such on to the surface of the inner walls of a polymerization reactor made of, for example, stainless steel followed by drying to fully exhibit the desired effect of polymer scale prevention. It is of course that the surfaces should have been cleaned in advance as far as possible by a conventional method in order to ensure uniform coating with the coating solution.
  • the means for coating is not limitative including spraying, brushing and other conventional methods.
  • the amount of coating is preferably at least 0.001 g/m 2 as dried to have fully exhibited effects of polymer scale prevention.
  • the reactor surfaces coated with the aqueous coating solution are then dried.
  • the wet surfaces are conveniently and rapidly dried by blowing with hot air heated at 40° to 100° C.
  • the reactor surfaces are heated in advance at 40° to 100° C. by a suitable means and the aqueous coating solution is directly applied on to the heated surface so as that coating is followed by drying.
  • the coated surface is preferably rinsed with water to remove any dissolvable matter leaving the coating films insolubilized by drying.
  • the reactor surface to be coated with aqueous coating solution in accordance with the present invention is undercoated in advance by a conventional coating solution used for the purpose of polymer scale prevention.
  • a conventional coating solution used for the purpose of polymer scale prevention.
  • Such an undercoating treatment is sometimes advisable when further improvement is desired for the reliability and durability of the coating films formed with the aqueous coating solution according to the invention to be effective in a number of repeated polymerization runs.
  • aqueous coating solution containing the components (a) and (b) as described above, however, difficulties are sometimes encountered in obtaining uniform and even spreading of the solution on the surface of, for example, stainless steel due to the high surface tension of the aqueous solution and poor affinity of the metal surface to the aqueous solution.
  • a conventional way of decreasing the surface tension of an aqueous solution is to add a surface active agent to the solution.
  • the addition of a surface active agent is, however, undesirable in this case since the presence of a surface active agent in the coating films on the reactor surfaces rather increases the polymer scale deposition contrary to the object of the inventive method.
  • aqueous coating solution with a small amount of an aliphatic monovalent lower alcohol having from 3 to 6 carbon atoms in a molecule.
  • alcohol compounds are n-propyl alcohol, isopropyl alcohol, n-butyl alcohol, isobutyl alcohol, sec-butyl alcohol, tert-butyl alcohol, n-amyl acohol, tert-amyl alcohol, isoamyl alcohol, sec-amyl alcohol, sec-hexyl alcohol and the like. They are used either singly or as a mixture of two kinds or more.
  • the concentration of the alcohol compound in the aqueous coating solution is desirably at least 1% by weight in order to obtain the desired effect to a significant extent while the upper limit of the concentration is not particularly limitative but usually not exceeding 20% by weight. It is optional to use an organic solvent readily miscible with water such as ester solvents and ketone solvents in combination with the alcohol in a limited amount.
  • the aqueous coating solution thus admixed with the alcohol is applied on to the reactor surfaces and dried just in the same manner as in the case of the coating solution without the addition of the alcohol. After completion of coating with the aqueous coating solution and drying, the polymerization run is undertaken in the thus treated polymerization reactor.
  • the procedure of the polymerization run per se is not particularly different from conventional runs and the reactor having the surfaces of the wall and other parts coming into contact with the monomer or monomers coated and dried as described above is charged with water as the aqueous polymerization medium, monomer or monomers, polymerization initiators and other ingredients to start the polymerization run.
  • an alkaline substance for reducing the polymer scale deposition particularly for the polymerization of vinyl chloride in an aqueous medium as is well known in the art.
  • an alkaline substance is exemplified by water-soluble compounds of alkali metals or alkaline earth metals including hydroxides, carbonates, hydrogencarbonates, silicates and acetates although the amount of such an alkaline substance should be limited not to adversely affect the properties of the polymer products.
  • the method of the present invention is very effective for various types of polymerization including not only suspension polymerization of vinyl chloride but also emulsion polymerization of vinyl chloride and polymerization of other ethylenically unsaturated monomers in an aqueous medium.
  • an emulsifying agent such as sodium laurylsulfate, sodium dodecylbenzenesulfonate, sodium dioctylsulfosuccinate and the like belonging to the class of anionic surface active agents and sorbitan monolaurate, polyoxyethylene alkyl ethers and the like belonging to the class of non-ionic surface active agents.
  • the effectiveness of the inventive method is relatively insusceptible to the influence of the kinds of the other ingredients such as suspending agents and polymerization initiators as well as several optional additive ingredients such as fillers, stabilizers, lubricants, chain transfer agents, plasticizers and the like.
  • a diversity of ethylenically unsaturated monomers can be polymerized in an aqueous medium with no or little depostion of polymer scale on the reactor surfaces treated in accordance with the inventive method.
  • the monomers applicable include vinyl halides such as vinyl chloride, vinyl esters such as vinyl acetate and vinyl propionate, acrylic acid and methacrylic acid and esters and salts thereof, maleic acid and fumaric acid and esters thereof, maleic anhydride, dienic monomers such as butadiene, chloroprene and isoprene, aromatic vinyl compounds such as styrene, unsaturated nitriles such as acrylonitrile, vinylidene halides such as vinylidene chloride and vinyl ethers such as vinyl ethyl ether.
  • the method of the present invention is particularly effective for the suspension polymerization or emulsion polymerization of vinyl halides such as vinyl chloride and/or vinylidene halides such as vinylidene chloride or copolymerization of a monomer mixture mainly composed of the vinyl halides and/or vinylidene halides.
  • the method of the present invention is applicable to the polymerization of styrene, methyl methacrylate and acrylonitrile in an aqueous medium as well as to the emulsion polymerization for the preparation of latices of synthetic rubbers such as SBR, NBR, CR, IR and IIR or ABS resins in a stainless steel polymerization reactor, which polymerizations being performed hitherto in glass-lined polymerization reactors due to the lack of an effective means for preventing scale deposition on the inner walls of a stainless steel polymerization reactor.
  • synthetic rubbers such as SBR, NBR, CR, IR and IIR or ABS resins
  • Aqueous coating solutions were prepared each by dissolving a water-soluble cationic polymer compound as the component (a) and a water-soluble anionic dye as the component (b) of the kinds as indicated in Table 1 below in water.
  • the amounts of the components (a) and (b) in each of the solutions were such that the total concentration of them was about 0.1% by weight, the weight ratio of the component (a) to the component (b) being as indicated in Table 1.
  • the aqueous coating solution was admixed with an alcohol compound of the kind indicated in the table in an amount also given in the same table.
  • the amount of addition of the alcohol given by parts by weight is per 100 parts by weight of the aqueous solution containing the components (a) and (b) as dissolved therein.
  • the thus prepared aqueous coating solution was applied by spray coating on to the surfaces of the inner walls of a polymerization reactor of 100 liter capacity and the stirrer thereof coming into contact with the monomer during the polymerization in a coating amount of 0.1-1.0 g/m 2 as dried followed by drying with heating at 50° C. for 15 minutes and washing with water.
  • Aqueous coating solutions were prepared each by dissolving a water-soluble cationic polymer compound as the component (a) and a water-soluble anionic dye as the component (b) of the kinds as indicated in Table 2 below in water.
  • the amounts of the components (a) and (b) in each of the solutions were such that the total concentration of them was about 0.1% by weight, the weight ratio of the component (a) to the component (b) being as indicated in Table 2.
  • isobutyl alcohol was added to the solution in an amount of 5.0 parts by weight per 100 parts by weight of the aqueous solution containing the components (a) and (b).
  • the thus prepared aqueous coating solution was applied by spray coating on to the surfaces of the inner walls of a stainless steel polymerization reactor of 120 liter capacity and the stirrer thereof coming into contact with the monomer in a coating amount of about 0.1-1.0 g/m 2 as dried followed by drying with heating at 90° C. for 10 minutes and thorough washing with water.
  • Aqueous coating solutions were prepared each by using a combination of a water-soluble anionic polymer compound as the component (a) and a water-soluble cationic dye as the component (b) of the kinds as indicated in Table 3 below.
  • the weight ratio of the component (a) to the component (b) is given in the table.
  • the total concentration of the components (a) and (b) was about 0.1% by weight in each of the experiments.
  • an alcohol compound was added to the aqueous solution as indicated in the table.
  • the amount of addition of the alcohol given in parts by weight in the table was per 100 parts by weight of the aqueous solution containing the components (a) and (b).
  • the thus prepared aqueous coating solution was applied by spray coating on to the surfaces of the inner walls of a polymerization reactor of 100 liter capacity and the stirrer thereof coming into contact with the monomer during the polymerization in a coating amount of 0.1-1.0 g/m 2 as dried followed by drying with heating at 50° C. for 15 minutes and washing with water.
  • Aqueous coating solutions were prepared each by dissolving an anionic polymer compound as the component (a) and a cationic dye as the component (b) of the kinds as indicated in Table 4 below in water.
  • the weight ratio of the component (a) to the component (b) in each of the solutions was as given in the table and the total concentration of the components (a) and (b) in the solution was about 0.1% by weight.
  • each of the solutions was admixed with 5 parts by weight of isobutyl alcohol per 100 parts by weight of the solution containing the components (a) and (b).
  • the thus prepared aqueous coating solution was applied by spray coating on to the surfaces of the inner walls of a stainless steel polymerization reactor of 120 liter capacity and the stirrer thereof coming into contact with the monomer in a coating amount of about 0.1-1.0 g/m 2 as dried followed by drying with heating at 90° C. for 10 minutes and thorough washing with water.
  • the inner walls and the stirrer of a stainless steel polymerization reactor of 400 liter capacity were coated with an aqueous coating solution prepared in Experiments No. 5, NO. 7, No. 9, No. 26 or No. 30 of Examples 1 or 4 in a coating amount of about 0.1-1.0 g/m 2 as dried followed by drying with heating at 50° C. for 30 minutes and thorough washing with water.
  • aqueous coating solution prepared in Experiments No. 5, NO. 7, No. 9, No. 26 or No. 30 of Examples 1 or 4 in a coating amount of about 0.1-1.0 g/m 2 as dried followed by drying with heating at 50° C. for 30 minutes and thorough washing with water.
  • Into the thus treated polymerization reactor were introduced 100 kg of vinyl chloride monomer, 120 kg of deionized water, 0.1 kg of potassium persulfate, 0.05 kg of disodium phosphate and 1.9 kg of sodium dodecylbenzenesulfonate and the emulsion polymerization of the monomer was carried out at
  • Example 5 The same polymerization reactor as used in Example 5 was coated with an aqueous coating solution prepared in Experiments No. 6, No. 8, No. 9, No. 28 or No. 30 of Examples 1 or 4 followed by drying and washing with water in the same manner as in Example 5.
  • Into the thus treated polymerization reactor were introduced 98.6 kg of deionized water, 100 kg of vinylidene chloride monomer, 7 kg of acrylonitrile monomer, 0.11 kg of ammonium persulfate, 0.11 kg of sodium hydrogensulfite, 0.64 kg of a polyoxyethylene alkyl ether, 0.05 kg of sodium dodecylbenzenesulfonate and 0.05 kg of acetic acid and emulsion copolymerization of the monomers was carried out at 50° C. for 9 hours with agitation.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polymerisation Methods In General (AREA)
  • Paints Or Removers (AREA)
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US06/149,414 1979-05-22 1980-05-13 Method for preventing polymer scale deposition in the polymerization of an ethylenically unsaturated monomer in an aqueous medium Expired - Lifetime US4272622A (en)

Applications Claiming Priority (4)

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JP54-62780 1979-05-22
JP6278079A JPS55155002A (en) 1979-05-22 1979-05-22 Polymerization of vinyl monomer
JP6476579A JPS55157602A (en) 1979-05-25 1979-05-25 Polymerization of vinyl monomer
JP54-64765 1979-05-25

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DE (1) DE3019390A1 (de)
FR (1) FR2457169A1 (de)
GB (1) GB2052302B (de)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4933399A (en) * 1987-12-08 1990-06-12 Shin-Etsu Chemical Co., Ltd. Method of preventing polymer-scale formation
US4996272A (en) * 1987-03-25 1991-02-26 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin used for magnetic recording media and a method for the production of the same
US5028676A (en) * 1989-06-26 1991-07-02 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin for magnetic recording media from vinyl chloride with quanternary and phosphoric monomers
US5130386A (en) * 1989-03-02 1992-07-14 Shin-Etsu Chemical Co., Ltd. Method of preventing polymer scale deposition during polymerization
US5142003A (en) * 1990-06-19 1992-08-25 Shin-Etsu Chemical Company, Limited Agents to prevent polymer scale deposition and a method therefor
US5244986A (en) * 1990-05-22 1993-09-14 Shin-Etsu Chemical Co., Ltd. Method of preventing polymer scale deposition
US5378775A (en) * 1991-05-17 1995-01-03 Shin-Etsu Chemical Co., Ltd. Polymer scale preventive agent, polymerization vessel for preventing polymer scale deposition, and process of producing polymer using said vessel
US6320001B1 (en) * 1999-04-08 2001-11-20 Shin-Etsu Chemical Co., Ltd. Process for producing a polymer by polymerization of a monomer having an ethylenic double bond
US6335403B1 (en) * 1999-06-25 2002-01-01 Shin-Etsu Chemical Co., Ltd. Process for producing a polymer by polymerization of a monomer having an ethylenic double bond
US6962608B1 (en) 2002-10-01 2005-11-08 The Regents Of The University Of California Regenerable antimicrobial polymers and fibers with oxygen bleaches

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03115305A (ja) * 1990-05-25 1991-05-16 Shin Etsu Chem Co Ltd 重合体スケールの付着防止方法および重合体スケール付着防止剤
DE69117368T2 (de) * 1990-07-16 1996-07-18 Shin-Etsu Chemical Co., Ltd., Tokio/Tokyo Mittel zur Verhinderung von Krustenbildung von Polymeren und Verfahren zur Verhinderung der Krustenbildung mittels diesen Mittels
CA2047077A1 (en) * 1990-07-16 1992-01-17 Masahiro Usuki Polymer scale preventive agent and method of preventing polymer scale deposition using it
CA2053827A1 (en) * 1990-10-23 1992-04-24 Toshihide Shimizu Polymer scale preventive composition
DE102008060175A1 (de) * 2008-11-28 2010-06-02 Kerona Gmbh Verfahren zur Verhinderung von Ablagerungen

Citations (1)

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US3669946A (en) * 1970-05-07 1972-06-13 Shinetsu Chemical Co Method for preparing polyvinyl chloride by suspension polymerization

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GB1444360A (en) * 1972-11-20 1976-07-28 Ici Ltd Vinyl chloride polymerisation process
US3849179A (en) * 1973-08-27 1974-11-19 Goodrich Co B F Internally coated reaction vessel and process for coating the same
JPS5153589A (en) * 1974-11-06 1976-05-12 Shinetsu Chemical Co Harogenkabiniruno kaijojugoho
JPS5224953B2 (de) * 1974-12-27 1977-07-05 Shinetsu Chemical Co
GR64894B (en) * 1977-01-25 1980-06-07 Shinetsu Chemical Co Method for the polymerization of a vinyl menomer

Patent Citations (1)

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US3669946A (en) * 1970-05-07 1972-06-13 Shinetsu Chemical Co Method for preparing polyvinyl chloride by suspension polymerization

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4996272A (en) * 1987-03-25 1991-02-26 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin used for magnetic recording media and a method for the production of the same
US5008357A (en) * 1987-03-25 1991-04-16 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin for magnetic recording media from vinyl chloride polymer with quaternary groups
US5037893A (en) * 1987-03-25 1991-08-06 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin used for magnetic recording media derived from vinyl chloride and quaternary monomer
US4933399A (en) * 1987-12-08 1990-06-12 Shin-Etsu Chemical Co., Ltd. Method of preventing polymer-scale formation
US5130386A (en) * 1989-03-02 1992-07-14 Shin-Etsu Chemical Co., Ltd. Method of preventing polymer scale deposition during polymerization
US5028676A (en) * 1989-06-26 1991-07-02 Sekisui Kagaku Kogyo Kabushiki Kaisha Resin for magnetic recording media from vinyl chloride with quanternary and phosphoric monomers
US5244986A (en) * 1990-05-22 1993-09-14 Shin-Etsu Chemical Co., Ltd. Method of preventing polymer scale deposition
US5142003A (en) * 1990-06-19 1992-08-25 Shin-Etsu Chemical Company, Limited Agents to prevent polymer scale deposition and a method therefor
US5378775A (en) * 1991-05-17 1995-01-03 Shin-Etsu Chemical Co., Ltd. Polymer scale preventive agent, polymerization vessel for preventing polymer scale deposition, and process of producing polymer using said vessel
US6320001B1 (en) * 1999-04-08 2001-11-20 Shin-Etsu Chemical Co., Ltd. Process for producing a polymer by polymerization of a monomer having an ethylenic double bond
US6335403B1 (en) * 1999-06-25 2002-01-01 Shin-Etsu Chemical Co., Ltd. Process for producing a polymer by polymerization of a monomer having an ethylenic double bond
US6962608B1 (en) 2002-10-01 2005-11-08 The Regents Of The University Of California Regenerable antimicrobial polymers and fibers with oxygen bleaches

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FR2457169B1 (de) 1982-10-08
DE3019390A1 (de) 1980-12-04
GB2052302B (en) 1983-04-07
FR2457169A1 (fr) 1980-12-19
DE3019390C2 (de) 1989-01-19
GB2052302A (en) 1981-01-28

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